EP0015132A1

EP0015132A1 - Crystalline zeolitic material, synthesis and use thereof

Info

Publication number: EP0015132A1
Application number: EP19800300463
Authority: EP
Inventors: Louis Deane Rollman; Ernest William Valyocsik; Pochen Chu
Original assignee: Mobil Oil Corp
Current assignee: ExxonMobil Oil Corp
Priority date: 1979-02-21
Filing date: 1980-02-19
Publication date: 1980-09-03
Also published as: NZ192909A; EP0015132B1; DE3066664D1; BR8001035A; CA1141357A

Abstract

A new crystalline zeolitic material, designated ZSM-48, the composition ofwhich expressed in terms of moles per 100 moles of silica, usually falls within the range:

(Oto 15)RN : (Oto1.5)M2/nO : (0-2)Al₂O₃: (100)SiO₂ wherein M is at least one cation having a valence n, RN is a C₁-C₂₀ organic compound, having at least one amine functional group of pKa≥7. ZSM-48 is characterized by the distinctive X-ray powder diffraction pattern shown in Table I, and is prepared from a reaction mixture comprising a source of silica, C₁-C₂₀ organic compounds as defined above, with or without a source of alumina, and water.

Description

This invention relates to a new crystalline zeolitic material, to a method for synthesising it, and to its use, inter alia as organic conversion catalyst.
Many crystalline zeolites are known, in most cases as aluminosilicates. Some occur (at least so far) only in nature, for instance paulingite and merlinoite; some occur only as a result of synthesis, for instance zeolites A and ZSM-5; and some occur in both natural and synthetic forms, for instance mordenite, a synthetic counterpart.of which is known as Zeolon, and faujasite, synthetic counterparts of which are known as zeolites X and Y. Counterparts are of course demonstrated as such by correspondence of their X-ray diffraction data, the indicia by means of which the individuality of a zolite is established. Such data are a manifestation of the particular geometry of the three-dimensional lattice, formed of SiO₄ and in most cases A10₄ tetrahedra crosslinked by the sharing of oxygen atoms and including sufficient cationic complement to balance the resulting negative charge on any A10₄ tetrahedra, of which a zeolite may consist.
The chemical formula of an aluminosilicate zeolite is thus
where M is a cation of valence n and x and y are the number of aluminum and silicon atoms, respectively, in the unit cell (the geometric unit which repeats throughout the extent of the lattice). This expression is however frequently transmuted into the "mole ratio of oxides" form,
which is of course empirically ascertainable and thus the only formula which can be ascribed to a zeolite when its unit cell contents are unknown. Since the only significant quantity in such a formula is the term 2y/x, and since this term (which is almost invariably a range) can usually be satisfied by many zeolites of widely differing lattice geometry, chemical formula is not uniquely restrictive in establishing the identity of a zeolite. Furthermore, such a formula frequently expresses artefact when empirically derived, the cationic-valence/aluminum-atoms ratio deviating from unity, and it fails to provide for zeolites whose lattice structure can be brought into existence from reaction mixtures from which alumina is excluded. Moreover, both the unit cell formula and the "mole ratio of oxides" formula imply that the geometrical identity which persists between succeeding unit cells is accompanied by their compositional identity.
We have now discovered a zeolite having a lattice structure previously unknown, as evidenced by its X-ray diffraction data, which we call ZSM-48.
According to the present invention a crystalline zeolitic material, ZSM-48, has a lattice constituted by SiO₄ and possibly AlO₄ tetrahedra crosslinked by the sharing of oxygen atoms and characterized by the following interplanar spacings:
These values were determined by standard techniques. The radiation was the K-alpha doublet of copper, and a scintillation counter spectrometer with a strip chart pen recorder was used. The peak heights, I, and t'be positions as a function of 2 times theta, where theta is the Bragg angle, were read from the spectrometer chart. From these, the relative intensities, 100 1/1₀, where I_o is the intensity of the strongest line or peak, and d (obs.), the interplanar spacing in A, corresponding to the recorded lines, were calculated. In Table 1 the relative intensities are given in terms of the symbols W= weak, VS = very strong, W-VS and W-M = weak to very strong and weak to medium respectively. The pattern is preserved upon ion exchanges, possibly with some minor shifts in interplanar spacing and variation in relative intensity. Other minor variations can occur depending on the silicon to aluminum ratio of the particular sample and its thermal history.
In the as-synthesised form ZSM-48 usually manifests the formula in terms of mole ratios of oxides:

(0 to 15) RN : (0 to 1.5)M₂/_n0 : (0 to 2)Al₂O₃ : (100)Si0₂

₁

₂₀

When the material contains tetrahedrally coordinated (framework) aluminum, a fraction of the amine functional groups may be protonated. The doubly protonated form, in conventional notation, would be (RNH)₂0 and is equivalent in stoichiometry to 2 RN + H₂O.
Any original cations can be replaced, at least in part, by calcination and/or ion exchange. Calcination will convert as-synthesised organic cations to protons. Exchange may be performed with a metal of Groups 2 through 8 of the Periodic Table or with hydrogen ions or precursors thereof such as ammonium. Catalytically active forms of ZSM-48 can result from exchange with hydrogen, rare earth metals, aluminum, and manganese.
ZSM-48 can be prepared from a reaction mixture containing a source of silica, RN, an alkali metal oxide, e.g. sodium, water, and optionally alumina, and having a composition, in terms of mole ratios of oxides, falling within the following ranges:

wherein RN is a C₁-C₂₀ organic compound having amine functional group of pK_a≥7, and maintaining the mixture at 80-250°C until crystals of the material are formed. H⁺(added) is moles acid added in excess of the moles of hydroxide added. In calculating H⁺(added) and OH values, the term acid (H⁺) includes both hydronium ion, whether free or coordinated, and aluminum. Thus aluminum sulfate, for example, would be considered a mixture of aluminum oxide, sulfuric acid, and water. An amine hydrochloride would be a mixture of amine and HC1.
ZSM-48 can be used as a catalyst in intimate combination with an additional component such as tungsten, vanadium, molybdenum, rhenium, nickel, cobalt, chromium, manganese, or a noble metal such as platinum or palladium where a hydrogenation-dehydrogenation function is to be performed. Such component can be introduced by exchange impregnation or physical intimate admixture, in known manner.
ZSM-48 when employed either as an adsorbent or as a catalyst should be dehydrated, at least partially, by heating to a temperature in the range of 100 to 600°C in an atmosphere, such as air; nitrogen, etc. and at atmospheric, subatmospheric or superatmospheric pressures for between 1 and 48 hours. Dehydration can also be performed at room temperature merely by placing the material in a vacuum, but a longer time is required to obtain a sufficient amount of dehydration.
Preferably, crystallization is carried out under pressure in an autoclave or static bomb reactor. Thereafter, the crystals are separated from the liquid and recovered. The reaction mixture is prepared from materials which supply the appropriate oxide. Such compositions include sodium silicate, silica hydrosol, silica gel, silicic acid, RN, sodium hydroxide, sodium chloride, aluminum sulfate, sodium aluminate, aluminum oxide, or aluminum itself. RN is a C₁-C₂₀ organic compound containing at least one amine functional group of pKa≥7 and includes such compounds as C₃-C₁₈ primary, secondary, and tertiary amines, cyclic amine, such as piperidine, pyrrolidine and piperazine, and polyamines such as NH₂-C_nH_2n-NH₂ wherein n is 4-12.
For catalytic usage ZSM-48 may be composited with a matrix such as described in our European Specification 0,001,695. The relative proportions of ZSM-48 and matrix vary widely with the content of zeolitic material ranging from about 1 to about 90 perent by weight and more usually, particularly when the composite is prepared in the form of beads, in the range of about 2 to about 70 percent by weight'of the composite.
Employing a catalytically active form of ZSM-48 containing a hydrogenation component, reforming stocks can be reformed employing a temperature between 300°C and 600°C. The pressure can be between 100 and 1000 psig but is preferably between 200 and 700 psig. The liquid hourly space velocity is generally between 0.1 and 10, preferably between 0.5 and 4 and the hydrogen to hydrocarbon mole ratio is generally between 1 and 20 preferably between 4 and 12.
ZSM-48 can also be used for hydroisomerization of normal paraffins, when provided with a hydrogenation component, e.g., platinum. Hydroisomerization is carried out at a temperature between 100° and 4000C, preferably 150° to 300°C, with a liquid hourly space velocity between 0.01 and 2, preferably between 0.25 and 0.50 employing hydrogen such that the hydrogen to hydrocarbon mole ratio is between 1:1 and 5:1. Additionally, the catalyst can be used for olefin or aromatic isomerization employing temperatures between' 50° and 400°C.
ZSM-48 can also be used as a catalyst for reducing the pourpoint of gas oils. This reduction is carried out at a liquid hourly space velocity between about 10 and about 30 and a temperature between about 400° and about 600°C. Other reactions which can be catalysed by it, with or without a metal, e.g., platinum, or palladium, include hydrogenation-dehydrogenation reactions and desulfurization reactions, olefin polymerization (oligomerization), aromatics alkylation with C₂-C₁₂ olefins or with C₁-C₁₂ alcohols, aromatics isomerization, disproportionation, and transalkylation and other organic compound conversion such as the conversion of alcohols (e.g. methanol) to hydrocarbon.
In the examples which follow ZSM-48 was prepared from reaction mixtures of the composition range:

(0.1 to 0.5)RN : (0.3 to 0.8)Na₂0 : (0 to 0.02)Al₂O₃ Si0_{2 :} (20 to 70)H ₂0

₁

₂₀

_a

Examples 1-17

A starting gel reaction mixture was prepared from sodium silicate (27.8% SiO₂, 8.4% Na ₂0, 64% H₂O), a C₃-C₁₂ diamine compound, sodium hydroxide and water. Crystallization was carried out with stirring in a stainless steel autoclave at 160°C. After crystallization, the solids were separated by filtration and then water washed followed by drying at about 100°C. The amounts of starting material, identification of same, product characterizations and reaction times are listed in Table 2.
The x-ray diffraction patterns of the products of Examples 5 and 7 are shown in Figures 1. and 2, respectively, and their numerical values are shown in Table 3 below. Analytical and sorption data of the products are listed in Table 4 set forth herein (Examples 18-25). Sorption was determined after dehydration at at least 200°C.
Review of the data in Table 2 shows that (1) no ZSM-48 crystallized in the-absence of the diamine. (Ex. 1) (2) C₄-C₁₀ diamines yielded ZSM-48 in good crystallinity (Ex. 3-9) (3) ZSM-48 can be prepared with added aluminum although with these diamines, ZSM-5 (Ex. 13) or ZSM-11 (Ex. 12) may be preferred, depending on reaction mixture composition, and (4) that an optimum OH/SiO₂ ratio exists near zero.

Example 26

This example shows that very different types of amines are effective in ZSM-48 synthesis. A reaction mixture was prepared as in Examples 1-17 except that the amine was N,N^l-bis(3-aminopropyl) piperazine. Mole ratio of reactants were as follows:
after 2 days at 160°C in a stirred autoclave, ZSM-48 was obtained in good crystallinity.

Example 27

This example shows that simple amines are effective in ZSM-48 synthesis. A reaction mixture was prepared according to the procedures of Examples 1-17 except that the organic was n-hexylamine. The reaction mixture composition had the following mole ratios:
Crystallization was conducted in a stirred autoclave at 160°C for 2 days. The crystalline product was ZSM-48, contaminated with a minor portion

Example 28

The product of Example 7 was tested for relative hexane cracking activity (
-value), and for constraint index (the ratio of the rate constant for cracking of n-hexane to that of 3-methylpentane) at 510 and at 538°C*. At 510°C, the ZSM-48 product exhibited a constraint index of 5.3 and an of 5.0. At 538°C, the C.I. was 3.4.
* The
-test is described in a letter to the editor entitled 'Superactive Crystalline Alupinosilicate Hydrocarbon Cracking Catalysts' by P.B. Weisz and J. N. Miale, Journal of Catalysis, Vol. 4, pp. 527-529 (August 1965). The constraint index test is described in U.S. Patent 4,107,224.
As previously mentioned, the X-ray diffraction pattern is preserved upon ion exchanges, possibly with minor shifts in spacing and variation in relative intensity. We have found that the calcined, sodium-exchanged form of ZSM-48 exhibits the following interplanarspacings:
The relative intensities are given by the same symbols as used in Table 1 above.
The effect of calcination and sodium exchange is illustrated by Examples 29 and 30 below.

Example 29

The dried product of Example 5 (two grams) was calcined in nitrogen for 2.5 hours at 550°C followed by cooling in nitrogen for about 30 minutes. The calcined sample was ion exchanged three times with stirring at 80°C with 100 ml 2N sodium nitrate, for 2 hours each time. The sodium form sample was filtered, washed with water and dried under a heat lamp for about 30 minutes.
The X-ray diffraction data of the calcined sodium- exchange form is given below in Table 6, and the X-ray scan is shown in Figure 3 of the accompanying drawings.

Example 30

Claims

1 A crystalline zeolitic material having a cartice comprising Si0₄ tetrahedra crosalinked by the sharing of oxygen atoms and characterized by the following interplanar spacings :

2. A crystalline zeolitie material according to claim 1 the lattice of which also comprises A10₄ tetrahedra.

3. A crystalling ceolitic material according to claim 1 or claim whict as the formula, in termsof mole ratios:

0-15 RN : 0-1.5 M₂/_n0 : 0-2 Al₂O₃ : 100 SiO₂ in which M is at least one cation of valance n and RF is compound having at least one amine functional an organic compound having at least one amine functional group of pk_a 7.

4. A crystalline zeolitic material according to claim 3 wherein RN is of the formula H₂N- C_xH_2x- NH₂ in which x is from 4 to 12.

5. A crystalline zeolitic material according to claim 3 wherein RN is of the formula C_xH_2x+1 - NH₂ in which x is from 1 to 20.

6. A crystalline zeolitic material according to any of claims 2 to 5 which contains hydrogen, ammonium or rare earth cations.

7. A crystalline zeolitic material according to any of claims 2 to 6 in which the molar ratio of silica to alumina is from 800 to 15000.

8. A method for preparing the crystalline zeolitic material clamed in claim 1 which comprises preparing a reaction mixture containing a source of a silica, an alkali metal oxide, RN, water and alumina, and having a composition, in terms of mole ratios of oxides, falling within the following ranges:

wherein RN is a C₁-C₂₀ organic compound containing amine functional groups of pk_a7 and maintaining said mixture at crystallization temperature until crystals are formed.

9. A method according to claim 8 wherein said reaction mixture has the composition:

10. A method according to claim 8 or claim 9 in which RN is of the formula H2N - ^Cx^H2x - NH₂ in which x is from 4 to 12.

11. A method according to claim 8 or claim 9 in which RN is of the formula G_xH_2x+1- NH₂ in which x is from 1 to 20.

12. A method according, to any of claims 8 to 11 in which said temperature is in the range 80 to 250°C.

13. A process of converting an organic charge which comprises contacting the charge under conversion conditions with a catalyst comprising the material claimed in any of claims 1 to 7.